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- W2052987164 abstract "A mathematical model has been developed to predict the dynamic behaviour of moving-bed coal gasification reactors. The model is limited to dry-ash product gasification reactors and incorporates the long-term transient effects associated with the coal bed. Short-term transients are approximated using the steady-state version of the equations. The model is used to study the transient response of the gasifier to changes in coal feed rate, oxygen flow rate, and steam flow rate. The effects of step changes in these variables on the product gas composition and temperature profiles within the reactor are given. The controllability of the gasifier when subject to typical disturbances is also examined." @default.
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- W2052987164 date "1983-04-01" @default.
- W2052987164 modified "2023-09-26" @default.
- W2052987164 title "Dynamic behavior of moving-bed coal gasifiers" @default.
- W2052987164 doi "https://doi.org/10.1021/i200021a008" @default.
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